Literature DB >> 35721926

High-Pressure-Limit Rate Coefficients for HO2 Elimination Reactions of Hydroperoxyalkenylperoxy Radicals based on the Reaction Class Transition State Theory.

XiaoHui Sun1,2, ZhenYu Pei1, ZeRong Li2.   

Abstract

Thermokinetic parameters and transport parameters are of great importance to the combustion model and the reaction rate rules are of great importance to construct the combustion reaction mechanism for hydrocarbon fuels. The HO2 elimination reaction class for hydroperoxyalkenylperoxy radicals is one of the key reaction classes for olefin, for which the rate coefficients are lacking. Therefore, the rate coefficients and rate rules of the HO2 elimination reaction class for hydroperoxyalkenylperoxy radicals are studied in this work. The reaction class transition state theory (RC-TST) is used to calculate the rate coefficients. In addition, the HO2 elimination reaction class of hydroperoxyalkenylperoxy radicals is divided into four subclasses depending upon the type of H-Cβ bond that is broken in the reactant molecules, and the rate rules are calculated by taking the average of rate coefficients from a representative set of reactions in a subclass. The calculated kinetics data would be valuable for the construction of the combustion reaction mechanism for olefin.
© 2022 The Authors. Published by American Chemical Society.

Entities:  

Year:  2022        PMID: 35721926      PMCID: PMC9202253          DOI: 10.1021/acsomega.2c01811

Source DB:  PubMed          Journal:  ACS Omega        ISSN: 2470-1343


Introduction

A detailed understanding of the combustion model of hydrocarbon fuels plays a key role in exploring the reduction of the emissions from pollutants during combustion and may lead to cleaner and more efficient strategies in automotive vehicle and fuel design.[1] Meanwhile, the detailed kinetic model of combustion or pyrolysis for hydrocarbon fuels is of great significance to study the ignition phenomena, reactive flows, and so on.[2−8] However, there has been little kinetic modeling for unsaturated hydrocarbon fuels[4,9,10] compared to the extensive studies for saturated hydrocarbon fuels. It is valuable to study the impact of the C=C double bond on the reaction mechanism of unsaturated hydrocarbon fuels through theoretical and experimental studies.[3,11−14] In general, a complete reaction mechanism is composed of two parts: one is the core mechanism, which involves reactions of small molecules with no more than 4 carbon atoms and are common for all hydrocarbons. The other part is the expanded mechanism, which involves reactions of large molecules; these reactions are always divided into different reaction classes according to the similarities of the potential energy surfaces along their reaction coordinates[15,16] and are constructed in a systematic way by software on the basis of the rate estimation rules.[3,17−27] In the generation of the reaction mechanism, a complete and reasonable reaction list, accurate thermokinetic parameters, and transport parameters are essential.[3,16,28] It is widely accepted that the reaction mechanism in the low-temperature region is complex due to the large number of species and elementary reactions.[1,3,29−34] Olefins are one of the important components of transportation fuels and important intermediates during the combustion process for alkanes.[11,35] Analogous to the low-temperature oxidation process for alkanes, olefins first undergo hydrogen extraction reaction to form alkenyl radicals (R•), followed by oxidation to produce alkenylperoxy radicals (ROO•). The hydroperoxyalkenyl radicals (•QOOH) are produced through the intramolecular H-shift of alkenylperoxy radicals (ROO•). Then, the •QOOH radicals add to a second oxygen molecule to produce •O2QOOH (hydroperoxyalkenylperoxy) radicals.[36,37] The main reaction paths for olefin are schemed in Figure , where R, R•, and Q represent the olefin molecules (CH2), alkenyl radicals (CH2), and a chain with 2 H-atoms replaced by olefin molecules (CH2), respectively. Nowadays, experimental measurements and mechanism studies for ethylene,[38−43] propene,[44−47] butene,[48−50] and other large olefins[51−53] are being undertaken, including low- and high-temperature kinetic schemes. Up to now, there have been some theoretical studies of alkanes and their radicals by RC-TST,[54] wherein the thermokinetic parameters for large molecular systems are obtained by a low-level ab initio method.
Figure 1

Reaction pathways of olefin.

Reaction pathways of olefin. For the HO2 elimination reaction of hydroperoxyalkenylperoxy radicals, the Cα–OO and H–CβCαOO bonds are broken. Similar to the work[1,16,28] on olefins and their radicals, the H–Cβ bonds in this work are divided into allylic C–H bonds (i.e., the C–H bond is attached to the α position of the C=C double bond) and vinylic C–H bonds (i.e., the C–H bond on the C=C double bond). Analogous to the classification method of alkanes and their radicals,[55] a carbon atom that connects with three hydrogen atoms is defined as a primary (“p”) section, and a carbon atom that connects with two hydrogen atoms and one hydrogen atom is defined as secondary (“s”) and tertiary (“t”) sections, respectively. The types of C–H bonds studied in this work include the secondary allylic C–H bonds, secondary alkylic C–H bonds, and tertiary vinylic C–H bonds, which are shown in Figure . It is worth noting that the tertiary vinylic C–H bonds are artificially divided into 1-tertiary vinylic C–H bonds and 2-tertiary vinylic C–H bonds to distinguish the different transition states formed from the tertiary vinylic C–H bonds. Among them, the 1-tertiary vinylic C–H bond has a CH2 group between it and the OO radicals, and the 2-tertiary vinylic C–H bond is directly linked to the vinyl CH group.
Figure 2

Types of C–H bonds in a reactant molecule: (a) secondary allylic C–H bond; (b) secondary alkylic C–H bond; (c) 1-tertiary vinylic C–H bond; and (d) 2-tertiary vinylic C–H bond.

Types of C–H bonds in a reactant molecule: (a) secondary allylic C–H bond; (b) secondary alkylic C–H bond; (c) 1-tertiary vinylic C–H bond; and (d) 2-tertiary vinylic C–H bond. It is well known that the reaction mechanisms are usually developed automatically by software based on the reaction rate rules.[56−60] In order to reduce the uncertainty of the rate rules, the reaction class is usually divided into different reaction subclasses according to the reaction characteristics for the subclasses. Then, the rate rules are calculated by taking the average of the rate coefficients from a representative set of reactions for each subclass. In this work, 38 reactions for the HO2 elimination reaction class of hydroperoxyalkenylperoxy radicals are chosen; the reaction list is listed in Table . It is worth noting that only the number of carbon atoms involved in the reactions ranging from four to six are studied in this work. In addition, these 38 reactions are divided into “secondary allylic”, “secondary alkylic”, “1-tertiary vinylic”, and “2-tertiary vinylic” reaction subclasses. The terms “s-allylic”, “s-alkylic“, “1-tv”, and “2-tv” are used to represent the different reaction subclasses in the below discussion of tables and figures, and their descriptions will not be repeated. The detailed reaction processes for four reaction subclasses are expressed in Figure , where “n” (n = 0,1,2,3), “m” (m = 0,1,2), “a” (a = 0,1,2,3,4), “b” (b = 2,3,4,5), “d” (d = 1,2,3), and “e” (e = 3,4,5) in the reactant molecules refer to the number of methylenes, with Ra, Rb, and Rc representing the hydrogen atoms or substitutes.
Table 1

List of Reactions

reaction subclassreactionreaction equation
s-allylicR1cis-HOOCH=CH(CH2)2OO → HOOCH=CHCH=CH2 + HO2
R2trans-HOOCH=CH(CH2)2OO → HOOCH=CHCH=CH2+HO2
R3cis-HOOCH2CH=CH(CH2)2OO → HOOCH2CH=CHCH=CH2 + HO2
R4trans-HOOCH2CH=CH(CH2)2OO → HOOCH2CH=CHCH=CH2 + HO2
R5cis-HOO(CH2)2CH=CH(CH2)2OO → HOO(CH2)2CH=CHCH=CH2 + HO2
R6trans-HOO(CH2)2CH=CH(CH2)2OO → HOO(CH2)2CH=CHCH=CH2 + HO2
R7cis-HOO(CH2)3CH=CH(CH2)2OO → HOO(CH2)3CH=CHCH=CH2 + HO2
R8trans-HOO(CH2)3CH=CH(CH2)2OO → HOO(CH2)3CH=CHCH=CH2 + HO2
s-alkylicR9cis-HOOCH=CH(CH2)3OO → HOOCH=CHCH2CH=CH2 + HO2
R10trans-HOOCH=CH(CH2)3OO → HOOCH=CHCH2CH=CH2 + HO2
R11cis-HOOCH2CH=CH(CH2)3OO → HOOCH2CH=CHCH2CH=CH2 + HO2
R12trans-HOOCH2CH=CH(CH2)3OO → HOOCH2CH=CHCH2CH=CH2 + HO2
R13cis-HOO(CH2)2CH=CH(CH2)3OO → HOO(CH2)2CH=CHCH2CH=CH2 + HO2
R14trans-HOO(CH2)2CH=CH(CH2)3OO → HOO(CH2)2CH=CHCH2CH=CH2 + HO2
R15cis-HOOCH=CH(CH2)4OO → HOOCH=CH(CH2)2CH=CH2 + HO2
R16trans-HOOCH=CH(CH2)4OO → HOOCH=CH(CH2)2CH=CH2 + HO2
R17cis-HOOCH2CH=CH(CH2)4OO → HOOCH2CH=CH(CH2)2CH=CH2 + HO2
R18trans-HOOCH2CH=CH(CH2)4OO → HOOCH2CH=CH(CH2)2CH=CH2 + HO2
R19cis-HOOCH=CH(CH2)5OO → HOOCH=CH(CH2)3CH=CH2 + HO2
R20trans-HOOCH=CH(CH2)5OO → HOOCH=CH(CH2)3CH=CH2 + HO2
1-tvR21cis-HOOCH=CHCH2OO → HOOCH=C=CH2 + HO2
R22trans-HOOCH=CHCH2OO → HOOCH=C=CH2 + HO2
R23cis-HOOCH2CH=CHCH2OO → HOOCH2CH=C=CH2 + HO2
R24trans-HOOCH2CH=CHCH2OO → HOOCH2CH=C=CH2 + HO2
R25cis-HOO(CH2)2CH=CHCH2OO → HOO(CH2)2CH=C=CH2 + HO2
R26trans-HOO(CH2)2CH=CHCH2OO → HOO(CH2)2CH=C=CH2 + HO2
R27cis-HOO(CH2)3CH=CHCH2OO → HOO(CH2)3CH=C=CH2 + HO2
R28trans-HOO(CH2)3CH=CHCH2OO → HOO(CH2)3CH=C=CH2 + HO2
R29cis-HOO(CH2)4CH=CHCH2OO → HOO(CH2)4CH=C=CH2 + HO2
R30trans-HOO(CH2)4CH=CHCH2OO → HOO(CH2)4CH=C=CH2 + HO2
2-tvR31cis-HOO(CH2)2CH=CHOO → HOO(CH2)2C≡CH + HO2
R32trans-HOO(CH2)2CH=CHOO → HOO(CH2)2C≡CH + HO2
R33cis-HOO(CH2)3CH=CHOO → HOO(CH2)3C≡CH + HO2
R34trans-HOO(CH2)3CH=CHOO → HOO(CH2)3C≡CH + HO2
R35cis-HOO(CH2)4CH=CHOO → HOO(CH2)4C≡CH + HO2
R36trans-HOO(CH2)4CH=CHOO → HOO(CH2)4C≡CH + HO2
R37cis-HOO(CH2)5CH=CHOO → HOO(CH2)5C≡CH + HO2
R38trans-HOO(CH2)5CH=CHOO → HOO(CH2)5C≡CH + HO2
Figure 3

Reaction process for different reaction subclasses: (a) s-allylic subclass; (b) s-alkylic subclass; (c) 1-tv subclass; and (d) 2-tv subclass.

Reaction process for different reaction subclasses: (a) s-allylic subclass; (b) s-alkylic subclass; (c) 1-tv subclass; and (d) 2-tv subclass.

Computational Details and Methods

Computational Details

All ab initio calculations are done using the Gaussian 09 package.[61] The geometry optimization and frequency calculation are performed at the B3LYP/6-31+G(d,p) level of theory. The Gaussian-4(G4) method is used as the high-level ab initio method. In order to validate the reliability of the G4 method, the single-point energies for reactants, products, and transition states for reactions R21 and R22 are calculated by the benchmark CCSD(T)/cc-pVTZ method.[62,63] In addition, a scaling factor of 0.95 is used to scale the wavenumbers obtained from the frequency analysis.[16,27] The intrinsic reaction coordinate (IRC) analysis is used to confirm the reaction process and the corresponding reactants and products of the transition state belonging to the reaction. All of the intrinsic reaction coordinate (IRC) plots are provided in Figure S1 in the supporting information. The illustration of the reaction coordinate changes from IRC for reaction R1 is shown in Figure . The low-frequency vibrations corresponding to the torsions of the single bonds for reactants, transition states, and products are considered in the calculation of the rate coefficients, wherein the one-dimensional (1-D) hindered internal rotors are used to treat the low-frequency vibrations.[62,64,65] The potentials are performed at the B3LYP/6-31+G (d,p) level by a relaxed scan with an interval of 10° for each internal rotation of the reactants and products. For the transition states, the internal rotor scans are only treated with the torsions of single bonds that are not fixed in the transition states. It is worth noting that when the torsion potential is greater than 10 kcal/mol, it is treated as harmonic vibration for the single bonds.[66] The ChemRate software[67] is used to calculate the rate coefficients, and they are fitted to three parameters (A, n, E) over the temperature range of 500 to 2000 K in increments of 100 K according to the modified Arrhenius expression k = A·T·exp (−E/RT), wherein T, R, E, n, and A are the temperature, gas constant, activation energy, temperature coefficient, and pre-exponential factor, respectively. For reactions with high reaction barriers, tunneling correction is often necessary, especially at low temperature. In this work, tunneling correction factors are calculated with an asymmetric Eckart potential.[68−70]
Figure 4

Intrinsic reaction coordinate (IRC) analysis for reaction R1.

Intrinsic reaction coordinate (IRC) analysis for reaction R1.

Computational Methods

The rate coefficients in the transition state theory[71] can be written as , wherein κ(T), σ, kB, T, h, Q≠, Q, ΔV≠, and R are the tunneling coefficient, reaction symmetry number, Boltzmann constant, temperature, Planck constant, partition functions of the transition state and the reactant, reaction barrier (i.e., the difference of the electronic energies between the transition state and the reactant), and ideal gas constant, respectively. The reaction class transition state theory (RC-TST) is widely used to calculate the rate coefficients at modest levels using the ab initio method for each reaction class.[60,72−76] The basic idea of the RC-TST theory is that the smallest size reaction in a reaction class is regarded as the main reaction, and its accurate rate coefficient km can be obtained by a high-level ab initio method or an experimental value; the other reactions in the reaction class are regarded as representative reactions and their rate coefficients kr need to be calculated. In RC-TST, the relationship between kr and km can be expressed as , wherein fκ, fσ, fQ, fv, and fHR are the transmission, symmetry number, partition function, potential energy, and hindered rotor factors, respectively. These factors are the ratio of the corresponding factors for representative reaction and main reaction. Truong and co-workers observed that the vibrational imaginary frequency of the transition state is a conserved quantity for different reactions in a reaction class and the partition function can be accurately calculated by a low-level ab initio method. More importantly, they found that the accurate potential energy factor can be calculated by a low-level ab initio method. Meanwhile, in the work of Wang et al.,[72] they propose an interpretation of the dependence of potential energy factor on the level of the ab initio method and extend the isodesmic reaction to the calculation of reaction barriers, reaction enthalpies, and rate coefficients when the main reaction and representative reaction can be combined into a single isodesmic reaction. They point out that the accurate reaction barriers and reaction enthalpies for a representative reaction are the sum of reaction barriers and reaction enthalpies calculated by a low-level ab initio method and the correction value, wherein the correction value is the difference of the reaction barrier and reaction enthalpy for the main reaction calculated by the high- and low-level ab initio methods, respectively. Similarly, the accurate rate coefficient for a representative reaction is equal to the rate coefficient of the representative reaction calculated by a low-level ab initio method time correction factor; the factor is exp [(−ΔΔV≠)/RT], in which ΔΔV≠ is the correction scheme for the reaction barrier from the main reaction.

Results and Discussion

Geometries of the Reaction Center for the Transition States

The reaction center for the HO2 elimination reaction is a five-membered ring in the transition states, and the atoms and bonds involved in the reaction center are shown in Figure , wherein “d” represents the bond length, “a” represents the bond angle, “R” represents the hydrogen or substituent group, C1 and C2 are reactive atoms, and “n” (n = 0,1,2,3,4,5) and “m” (m = 0,1,2,3,4,5) represent the number of methylene radicals attached to the carbon atoms at the left and right ends of the C=C double bond in the reactant molecules, respectively. The optimized geometrical parameters of the reaction centers for the transition states are listed in Table S1 in the Supporting Information. The difference values of the geometrical parameters between the main reaction and representative reaction for each subclass are listed in Table S2 in the Supporting Information. The average values and maximum absolute deviation of the geometrical parameters for all reactions in each subclass of the transition states are listed in Table . The maximum absolute value of the difference in geometrical parameters between the main reaction and representative reaction are also listed in Table .
Figure 5

Geometries of the reaction center for the transition states (TS) of different reaction subclasses: (a) s-allylic subclass; (b) s-alkylic subclass; (c) 1-tv subclass; and (d) 2-tv subclass.

Table 2

Geometrical Parameters of the Reaction Center for the Transition States of Each Subclass

subclass d1a1/(°)d2a2/(°)d3a3/(°)d4a4/(°)d5a5/(°)
s-allylicaavg1.2899.601.3097.481.34151.861.4093.162.1597.82
bmad0.001.230.010.340.012.500.000.380.060.99
cmax0.000.720.010.280.011.350.000.270.030.70
s-alkylicavg1.2897.881.2997.731.34154.261.3993.272.2296.69
mad0.000.300.010.120.010.610.000.130.010.21
max0.000.250.010.100.010.590.000.130.010.18
1-tvavg1.2897.541.2499.011.37153.511.3796.732.2794.03
mad0.034.750.061.080.053.940.011.580.233.61
max0.034.370.061.080.056.060.011.580.223.61
2-tvavg1.2897.191.2597.471.37150.511.2596.732.1998.11
mad0.000.240.010.300.010.630.000.190.010.19
max0.000.240.010.300.010.630.000.190.010.13

The average value of the geometric parameters for the transition states of all reactions in each subclass.

The maximum absolute deviation between the different reactions in each subclass.

The maximum absolute value of the difference between the main reaction and representative reaction.

Geometries of the reaction center for the transition states (TS) of different reaction subclasses: (a) s-allylic subclass; (b) s-alkylic subclass; (c) 1-tv subclass; and (d) 2-tv subclass. The average value of the geometric parameters for the transition states of all reactions in each subclass. The maximum absolute deviation between the different reactions in each subclass. The maximum absolute value of the difference between the main reaction and representative reaction. From Table , it can be seen that the maximum absolute deviations for each subclass of bond lengths and bond angles are 0.06 Å and 2.50°, 0.01 Å and 0.61°, 0.23 Å and 4.75°, and 0.01 Å and 0.63°, respectively. The maximum absolute values of the difference between the main reaction and representative reaction are 0.03 Å and 1.35°, 0.01 Å and 0.59°, 0.22 Å and 6.06°, 0.01 Å and 0.63°. These results show that the geometries of the reaction centers for the transition states of “s-alkylic” and “2-tv” subclasses are conserved.

Reaction Barriers and Enthalpies

Validation of the Reaction Barriers

In this work, the G4 method is chosen as the high-level ab initio method in the correction scheme. To validate the reliability of the reaction barriers, reactions R21 and R22 from Table are selected to compare the reaction barriers by the G4 method and the benchmark CCSD(T)/cc-pVTZ method.[62,63] The results are listed in Table .
Table 3

Reaction Barriers by the G4 Method and CCSD(T)/cc-pVTZ Method (kcal/mol)a,b

 ΔV
reactionG4CCSD(T)/cc-pVTZΔV
R2145.5345.170.36
R2245.7446.36–0.62

ΔV≠′ the difference of reaction barriers between the G4 and CCSD(T)/cc-pVTZ methods.

ΔV≠ = ΔV≠(G4)-ΔV≠ (CCSD(T)/cc-pVTZ).

ΔV≠′ the difference of reaction barriers between the G4 and CCSD(T)/cc-pVTZ methods. ΔV≠ = ΔV≠(G4)-ΔV≠ (CCSD(T)/cc-pVTZ). It can be seen from Table that the reaction barriers for reactions R21 and R22 by the G4 method are close to those of the CCSD(T)/cc-pVTZ method, where the difference of reaction barriers is 0.36 and −0.62 kcal/mol, respectively.

Reaction Barriers and Enthalpies for the Main Reaction of Each Subclass

In this work, reactions R1, R9, R21, and R31 are chosen as the main reactions for each subclass and the other reactions in Table are chosen as representative reactions. The reaction barriers and enthalpies for the main reaction at B3LYP and G4 levels, and the difference between the B3LYP and G4 methods of each subclass are listed in Table .
Table 4

Reaction Barriers and Enthalpies for Each Subclass of the Main Reaction (kcal/mol)

  aΔV
bΔΔVcΔH
dΔΔH
reaction subclassreactionG4B3LYP G4B3LYP 
s-allylicR131.4628.962.5015.9912.503.49
s-alkylicR934.6831.493.1920.6918.332.36
1-tvR2145.5341.773.7633.4529.923.53
2-tvR3147.0446.600.4431.7133.08–1.37

ΔV≠ reaction barriers.

ΔΔV≠ the difference of reaction barriers between the G4 and B3LYP methods.

ΔH≠ reaction enthalpies.

ΔΔH≠ the difference of reaction enthalpies between the G4 and B3LYP methods.

ΔV≠ reaction barriers. ΔΔV≠ the difference of reaction barriers between the G4 and B3LYP methods. ΔH≠ reaction enthalpies. ΔΔH≠ the difference of reaction enthalpies between the G4 and B3LYP methods. It can be seen from Table that the corrected values of the reaction barrier for each subclass are 2.50, 3.19, 3.76, and 0.44 kcal/mol, respectively. The corrected values of the reaction enthalpy for each subclass are 3.49, 2.36, 3.53, and −1.37 kcal/mol, respectively.

Reaction Barriers and Enthalpies for the Representative Reaction

In this part, the reaction barriers and enthalpies for 10 representative reactions are calculated at B3LYP, G4 levels and the corrected value based on RC-TST. The results are listed in Tables and 6. All corrected reaction barriers and enthalpies are listed in Table S3 in the Supporting Information.
Table 5

Comparison of the Reaction Barriers (kcal/mol)

 ΔV
reactionG4B3LYPaΔ (DFT)bRC-TSTcΔ (RC-TST)
R233.5530.992.5633.500.05
R1034.3931.872.5235.05–0.66
R2245.7441.704.0445.450.29
R3246.8246.680.1447.12–0.30

difference between the G4 and B3LYP methods.

the results corrected by RC-TST.

difference between G4 and RC-TST.

Table 6

Comparison of the Reaction Enthalpies (kcal/mol)

 ΔH
reactionG4B3LYPaΔ (DFT)bRC-TSTcΔ (RC-TST)
R215.6612.133.5315.620.04
R1019.4917.472.0219.83–0.34
R2233.5230.173.3533.70–0.18
R3231.6133.27–1.6631.90–0.29

difference between the G4 and B3LYP methods.

the results corrected by RC-TST.

difference between G4 and RC-TST.

difference between the G4 and B3LYP methods. the results corrected by RC-TST. difference between G4 and RC-TST. difference between the G4 and B3LYP methods. the results corrected by RC-TST. difference between G4 and RC-TST. It can be seen from Tables and 6 that the absolute values of differences for the reaction barriers and enthalpies by the B3LYP and G4 methods are between 0.14–4.04 and 1.66–3.53 kcal/mol, respectively. However, the differences between the corrected reaction barriers and enthalpies by the RC-TST and G4 methods are reduced to 0.15–0.66 and 0.04–0.34 kcal/mol, respectively.

High-Pressure-Limit Rate Coefficients and Rate Rules

High-Pressure-Limit Rate Coefficients

In this paper, the rate coefficients are compared between the G4 method and RC-TST, which are among the high-level ab initio methods and are widely used in the study of the thermochemical properties of different compounds and the study of the kinetics of different reactions.[73] The rate coefficients for reactions R22, R23, R24, and R32 are listed in Table S4 in the Supporting Information. For illustration, Figure shows the difference of the rate coefficients for reactions R22, R23, R24, and R32.
Figure 6

Comparison of the rate coefficients for (a) R22, (b) R23, (c) R24, and (d) R32.

Comparison of the rate coefficients for (a) R22, (b) R23, (c) R24, and (d) R32. The average ratios of the rate coefficients by the G4 method and RC-TST are 2.76, 0.94, 0.46, and 0.06 between 500–2000 K for reactions R22, R23, R24, and R32, respectively, wherein a large deviation factor of 16.67 of the rate coefficients for “2-tv” subclasses is observed, for which the geometries of the reaction centers for the transition states are conserved. In order to study the impact of the C=C double bond of the reactant molecules on the rate coefficients, the rate coefficients in the temperature range of 500–1500 K for the saturated hydroperoxyalkylperoxy radicals from reference[77] and for the unsaturated hydroperoxyalkenylperoxy radicals in this work are compared. The results are listed in Table S5 in the Supporting Information. Figure shows the difference of the rate coefficients.
Figure 7

Comparison of the rate coefficients for saturated hydroperoxyalkylperoxy radicals and unsaturated hydroperoxyalkenylperoxy radicals.

Comparison of the rate coefficients for saturated hydroperoxyalkylperoxy radicals and unsaturated hydroperoxyalkenylperoxy radicals. It can be seen from Figure that the rate coefficients for the HO2 elimination reaction of saturated hydroperoxyalkylperoxy radicals are larger than the rate coefficients for unsaturated hydroperoxyalkenylperoxy radicals. The rate coefficients show a similar trend with temperature for the HO2 elimination reactions of saturated hydroperoxyalkylperoxy radicals and unsaturated hydroperoxyalkenylperoxy radicals, in which the rate coefficients increase with increase in the temperature. However, the difference is that the rate coefficients of the unsaturated hydroperoxyalkenylperoxy radicals increase more slowly than those of saturated hydroperoxyalkylperoxy radicals when the temperature is higher than 1000 K. In addition, the rate coefficients in the temperature range of 500–2000 K of the HO2 elimination reaction between the alkenylperoxy radicals from reference[78] and the hydroperoxyalkenylperoxy radicals in this work are also compared. The results are listed in Table S6 in the Supporting Information. Figure plots the comparison of the rate coefficients. In Figure , the CH2=CHCH2OO• and CH2=CH(CH2)3OO• radicals from reference[78] are represented by 1-RO2 and 2-RO2, respectively. The HOOCH=CHCH2OO• and HOOCH=CH(CH2)3OO• radicals in this work are represented by 1-O2QOOH and 2-O2QOOH, respectively.
Figure 8

Comparison of the rate coefficients for alkenylperoxy radicals and hydroperoxyalkenylperoxy radicals.

Comparison of the rate coefficients for alkenylperoxy radicals and hydroperoxyalkenylperoxy radicals. It can be seen from Figure that the rate coefficients for the HO2 elimination reaction of alkenylperoxy radicals are larger than the rate coefficients of hydroperoxyalkenylperoxy radicals. However, the impact of the molecular size on the rate coefficients of hydroperoxyalkenylperoxy radicals is different from that for the rate coefficients of alkenylperoxy radicals. When the temperature is higher than 1500 K, the rate coefficients tend to change gently with the molecular size. Therefore, the study of the HO2 elimination reaction for hydroperoxyalkenylperoxy radicals will be of great significance for understanding the impact of molecular size on the reaction reactivity between one-step and two-step oxygenation in the low-temperature reaction mechanism of alkenyl radicals. In this work, the impact of configurations of the reactant molecules on the rate coefficients is also considered; the comparison of the average rate coefficients for the cis- and trans-configuration reactant molecules of each subclass at 500, 1000, 1500, and 2000 K is shown in Table S7 in the Supporting Information. For illustration, Figure shows the impact of configurations of the reactants on the rate coefficients.
Figure 9

Comparison of the average rate coefficients of cis- and trans-hydroperoxyalkenylperoxy radicals.

Comparison of the average rate coefficients of cis- and trans-hydroperoxyalkenylperoxy radicals. It can be seen from Figure that the average rate coefficients of cis-hydroperoxyalkenylperoxy radicals are larger than the average rate coefficients of trans-hydroperoxyalkenylperoxy radicals for “s-allylic”, “s-alkylic”, and “1-tv” subclasses. However, the average rate coefficients of trans-hydroperoxy-alkyl-peroxy radicals are larger than the average rate coefficients of cis-hydroperoxy-alkyl-peroxy radicals for the “2-tv” subclass. In addition, the impact of the types of C–H bonds on the rate coefficients is shown in Figure . It can be seen from Figure that when the temperature is lower than 1000 K, the high-pressure-limit rate coefficients exhibit the following tendency: “s-allylic”> “s-alkylic”> “2-tv”> “1-tv”; when the temperature range is 1000–1200 K, the rate coefficients exhibit the following tendency: “s-allylic”>“2-tv”> “s-alkylic”> “1-tv”; when the temperature is larger than 1200 K, the high-pressure-limit rate coefficients exhibit the following tendency: “2-tv”> “s-allylic> “s-alkylic”> “1-tv”.
Figure 10

Comparison of the average rate coefficients for different subclasses at 500–2000 K.

Comparison of the average rate coefficients for different subclasses at 500–2000 K.

High-Pressure-Limit Rate Rules

The reaction rate rules in the high-pressure limit for each subclass are derived by taking the average of the rate coefficients from a representative set of reactions with different numbers of carbon atoms. The fitted (A, n, E) parameters in the high-pressure limit from 500 to 2000 K for all reactions are listed in Table . Meanwhile, the ratio f at 1000 K is used to evaluate the uncertainty of the rate rules.
Table 7

High-Pressure-Limit Rate Rules for the HO2 Elimination Reaction

  modified Arrhenius parameters
1000 K
reaction subclassreactionA (s–1)nE (kcal/mol)af
s-allylic 4.90 × 1044–10.7142.50 
R18.32 × 1044–9.6740.541.46
R22.34 × 1044–10.3944.130.50
R34.79 × 1044–10.7840.900.44
R44.68 × 1044–10.6642.480.51
R54.57 × 1044–10.9239.410.41
R69.33 × 1044–11.2340.440.06
R71.45 × 1045–10.9637.642.48
R81.20 × 1045–10.9038.532.13
s-alkylic 4.68 × 1044–10.7743.42 
R96.31 × 1044–10.5142.472.66
R104.68 × 1044–10.5342.821.47
R114.79 × 1044–11.1041.230.07
R128.91 × 1044–11.0741.980.12
R131.32 × 1045–11.0139.441.03
R147.59 × 1044–10.9740.060.59
R155.01 × 1044–10.9140.870.34
R161.10 × 1045–11.1541.240.12
R176.31 × 1044–10.9438.581.09
R181.26 × 1045–10.9738.801.62
R191.02 × 1045–10.9438.561.84
R209.12 × 1044–11.0038.601.06
1-tv 5.13 × 1044–10.6550.31 
R217.41 × 1038–8.4853.690.69
R224.79 × 1035–7.8851.900.06
R235.01 × 1044–10.5353.450.47
R244.17 × 1044–10.4454.600.42
R254.79 × 1044–10.6450.361.68
R267.94 × 1044–10.7752.410.42
R271.95 × 1045–11.5649.780.02
R282.09 × 1045–11.3850.230.06
R291.20 × 1045–11.0045.685.70
R302.34 × 1045–11.3647.090.46
2-tv 2.04 × 1045–10.3353.05 
R316.17 × 1044–9.8858.620.30
R327.76 × 1044–9.8957.010.93
R331.78 × 1045–10.2356.090.44
R342.09 × 1045–10.2554.700.86
R356.92 × 1044–10.8853.130.01
R362.14 × 1045–10.6851.630.27
R371.66 × 1045–10.4650.302.66
R384.07 × 1044–10.3549.022.53

f = k/kavg for each subclass; kavg is the average rate coefficient for the reactions in each subclass.

f = k/kavg for each subclass; kavg is the average rate coefficient for the reactions in each subclass. It can be seen from Table that the ranges of the ratio for each subclass are within 0.06–2.48, 0.07–2.66, 0.02–5.70, and 0.01–2.66 for the “s-allylic” subclass, “s-alkylic” subclass, “1-tv” subclass, and “2-tv” subclass, respectively. This indicates that the rate rules obtained by taking the average of the rate coefficients from representative reactions have a large deviation.

Conclusions

In this work, we report the reaction barriers, enthalpies, and rate coefficients for the HO2 elimination reaction of hydroperoxyalkenylperoxy radicals based on RC-TST. The high-pressure-limit rate coefficients and rate rules at 500–2000 K are calculated for the reaction class. The deviations of the reaction barriers and enthalpies for reactions R2, R10, R22, and R32 between B3LYP/6-31+G(d,p) and G4 methods are more than 1 kcal/mol, while the deviations are reduced to less than 1 kcal/mol after correction by the RC-TST method. Meanwhile, the deviation factor of rate coefficients for reaction R32 of “2-tv” subclasses is 16.67, which indicates that the geometries of the reaction centers for the transition states are conserved. In addition, the ranges of the uncertainty factor for the rate rules are within 0.06–2.48, 0.07–2.66, 0.02–5.70, and 0.01–2.66 for “s-allylic”, “s-alkylic”, “1-tv”, and “2-tv” subclasses, respectively, indicating that there is a large uncertainty in the rate rules by taking the average of rate coefficients for the representative reactions in the reaction subclass. Through the comparison of rate coefficients for saturated hydroperoxyalkylperoxy radicals and unsaturated hydroperoxyalkenylperoxy radicals, the results show that the C=C double bond on the rate coefficients of unsaturated hydroperoxyalkenylperoxy radicals increases more slowly than that of saturated hydroperoxyalkylperoxy radicals when the temperature is higher than 1000 K. The impact of the molecular size on the rate coefficients for alkenylperoxy radicals and hydroperoxyalkenylperoxy radicals is that the rate coefficients tend to change gently with the molecular size when the temperature is higher than 1500 K. Therefore, it is necessary to study the HO2 elimination reaction for the hydroperoxyalkenylperoxy radicals. In addition, the impact of configurations of the reactants on the rate coefficients exhibits the following tendency: k(cis)> k(trans) for “s-allylic”, “s-alkylic”, and “1-tv” subclasses, while k(trans)> k(cis) for the “2-tv” subclass. At the same time, the rate coefficients of the different types of C–H in the different temperature ranges show the following trend: “s-allylic”> “s-alkylic”> “2-tv”> “1-tv” (T<1000 K), “s-allylic”> “2-tv”> “s-alkylic”> “1-tv” (1000 K “s-allylic”> “s-alkylic”> “1-tv” (T>1200 K).
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